Group separations of lanthanides
from minor actinides is required
in the currently considered scenarios for closing of the nuclear fuel
cycle. TALSPEAK is a well-known and historically first process suggested
for such separations. The process is based on competitive complexation
of trivalent f-group ions by an aminopolycarboxylate
(such as the base of diethylenetriamine-N,N,N′,N″,N″-pentaacetic acid, DTPA) in an aqueous buffer and
a dialkylphosphate (such as the base of bis(2-ethylhexyl)phosphoric
acid, HDEHP) in an organic phase. Unfortunately, this method exhibits
excessive sensitivity to pH and composition of the aqueous feed. In
this study, we ″reinvent″ TALSPEAK, retaining the competitive
ion binding but changing considerably the chemical implementation
of the underlying general principles. The DTPA moiety is integrated
into a functionalized ionic liquid (IL) that is immiscible with an
organic phase containing dialkylphosphate ligands. Choline and betainium
bistriflimides double as IL diluents and synthetic reagents. The integration
of the aminopolycarboxylate moiety into these ILs is achieved in situ through the reactions of the cyclical dianhydride
of DTPA with IL functional groups, either through the formation of
a mixed dianhydride (for the betainium cation) or a diester (for the
choline cation). The deprotonated DTPA–betainium conjugate
forms 1:1 complexes with trivalent f-element cations
whereas these metal ions form 1:2 complexes with the DTPA–choline
conjugates. Large separation factors for Eu/Am partitioning between
the two phases are observed, approaching 120–150 for DTPA–betainium
and 250–270 for DTPA–choline. In the latter system,
as in the traditional aqueous TALSPEAK, there is a characteristic
″parabolic″ dependence of the phase distribution ratios
as a function of ionic radius that allows separations of the largest
lanthanide ions. Group separations of all lanthanides from americium
has been demonstrated, and a separation process that is based on this
chemistry is suggested.